GeorgeGrande
Chemical
- Jun 17, 2006
- 32
This is the case i am dealing with:
A 2" pipe connecting a pressure vessel (200.5 psia) to a pump. The pump is designed to fill and evacuate the cold and not pressurized fluid. I must protect the pump from 145 psia. In case of leaking (or open from some reson) 2" valve there will be high pressure flow to the pump.
I took worst case scenario for gas flowing through 2" pipe in sonic velocity and calculated the volume flow from pipe flow area and the velocity.
I am getting very large PSV for 2" pipe.
P=200.5 psia
T=287 oF
Tb= 97oF @ atm.
Vsonic=164 m/s
A 2" pipe connecting a pressure vessel (200.5 psia) to a pump. The pump is designed to fill and evacuate the cold and not pressurized fluid. I must protect the pump from 145 psia. In case of leaking (or open from some reson) 2" valve there will be high pressure flow to the pump.
I took worst case scenario for gas flowing through 2" pipe in sonic velocity and calculated the volume flow from pipe flow area and the velocity.
I am getting very large PSV for 2" pipe.
P=200.5 psia
T=287 oF
Tb= 97oF @ atm.
Vsonic=164 m/s